Rerefining used oil with borohydride reducing agents
Used oil is rerefined utilizing borohydride reducing agents. The borohydride reducing agent contacts the used oil in an aqueous solution, for example. Contact with the borohydride reducing agent may occur before, during or after distillation or evaporation of the used oil. The disclosed method reduces the concentration of carbonyl compounds and metals and reduces the corrosion characteristics of used oil.
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This invention relates to the rerefining of used oil. More particularly, this invention relates to the rerefining of used oil utilizing borohydride reducing agents for removing contaminants present in the oil as a result of being used.
BACKGROUND OF THE INVENTIONWaste oils have generally been disposed of by incineration, in landfill, or used in road oiling for dust control, because the cost of reclamation and rerefining has been excessive. However, because of the rising cost of hydrocarbon fuels and lubricants, coupled with the ever-increasing demand and depletion of resources, the need for an efficient, low-cost waste oil rerefining process has arisen.
Large and increasing volumes of used oil, such as crank- case oils from diesel and internal combustion engines, cutting oil, hydraulic oil, and other oils are produced each year. These waste oils may be contaminated with oxidation and degradation products, water, fine particulates, metal and carbon and oil additive products and other contaminants not found in virgin oil. Many of these contaminants are formed from the degradation of the oil when used or are contaminants from use which become added to the oil. These contaminants can render the oils unsuitable for continued use. Thus, the considerations and problems in connection with rerefining used oil are different from those associated with the refining of virgin oil, since used oil contains contaminants not present in crude oil.
In recent years some small scale rerefining processes have been put into operation in which marketable oils are recovered. However, due to the high costs involved and the resulting narrow margin of profit, such recovery processes represent a small percentage utilization of the total quantity of used oils.
The ever-increasing scarcity and consequent high costs of petroleum, particularly high quality stocks, now presents positive incentives to selectively remove undesirable contaminants from used oils and reuse the valuable high quality components contained in such oils.
Several waste oil rerefining processes are known from the prior art. For example, in U.S. Pat. No. 3,639,229, a process is described where a mixture of an aliphatic monohydric alcohol of from four to five carbon atoms and a light hydrocarbon is added to waste oil. The mixture settles into three distinct layers. The upper oily layer is recovered, treated with sulfuric acid and thereafter refined by conventional means.
In U.S. Pat. No. 3,919,076, a process is described that involves removing water from the waste oil, adding a saturated hydrocarbon solvent, settling the mixture to recover the oil/solvent mix, removing the solvent, vacuum distilling the residual oil to collect selected fractions, hydrogenating the fractions over a catalyst, stripping hydrogenated oil to remove light ends and filtering the remaining product.
U.S. Pat. No. 4,124,492 discloses a process for reclaiming useful hydrocarbon oil from contaminated waste oil in which the waste oil is dehydrated and, thereafter, the dehydrated oil is dissolved in selected amounts of isopropanol. The undissolved waste matter is separated and the residual oil/solvent fraction is distilled to recover the decontaminated oil and solvent. The recovered oil is further clarified by treatment with a bleaching clay or activated carbon at elevated temperatures.
In U.S. Pat. No. 4,021,333, a process is described for rerefining used oil that includes distilling a volatile forecut from the oil, followed by a conventional type of distillation that may occur at reduced pressure. Use of demister means is preferred to minimize carry-over of material into the distillate. The distillation is continued until the desired recovery is obtained. The impurities present in the distillate are extracted.
A need exists for a method of effectively removing or otherwise eliminating undesirable contaminants found in used oil to make the rerefined oil more suitable for use in, for example, internal combustion engines. Further, a need exists for such a method that is feasible for use on a commercial scale.
DISCLOSURE OF THE INVENTIONIn accordance with the present invention, a method is provided for rerefining used oil. The invention is particularly suitable for rerefining or treating lubricating oil, cutting oil, hydraulic oil, industrial oil, fuel oil, diesel oil, vegetable oil, synthetic oil and grease. As used herein, the term oil means any oil or grease that is capable of commercial use. The method in accordance with the present invention reduces the concentration of metals, carbonyl compounds and other contaminants which may be present in the oil from use, such as use in internal combustion engines and the like, for example. In addition, the method reduces the corrosion characteristics of the oil, thereby making the oil more suitable for reuse. Further, the color, odor, oxidation stability and thermal stability of the oil are improved. When combined with distillation or evaporation purification of the used oil, the distillation or evaporation curve is lowered, thereby providing a greater amount of overhead product at a given temperature. Thus, more of the used oil can be recovered without resorting to higher temperatures, resulting in an energy savings and helping to avoid coking and cracking of the oil and fouling of equipment. Other advantages include a treated used oil having a lower neutralization number and a higher flash point.
Thus, in one aspect, the present invention relates to increasing the yield of recovered oil without subjecting the waste oil feedstock to temperatures that create conditions of coking, cracking, or fouling. In another aspect, this invention relates to a process for reducing the concentration of metals and carbonyl compounds present in used oil, while reducing the corrosion characteristics of the used oil, improving color, odor, neutralization number, oxidation stability and thermal stability. Still another aspect of this invention relates to reducing the distillation or evaporation temperature while achieving the desired recovery of oil from the waste oil feedstock.
In accordance with the present invention, a method of reducing the concentration of metals, carbonyl compounds and other contaminants present in the used oil from use, reducing corrosion characteristics of the used oil and improving other characteristics of the oil, includes contacting the used oil with at least one borohydride reducing agent. Contact is maintained for a sufficient time to cause reaction and/or removal of contaminants from the oil.
The used oil may be maintained at an elevated temperature during contact with the borohydride reducing agent, the elevated temperature being below the decomposition temperature of the borohydride reducing agent. The preferred borohydride reducing agent is an alkali metal borohydride and more particularly is selected from the group consisting of sodium borohydride, potassium borohydride and mixtures thereof.
The method of the present invention generally is used as part of a process for rerefining used oil which may include distillation or evaporation of the used oil either before, during and/or after contact with the borohydride reducing agent. Thus, the borohydride reducing agent may be added to a distillation column, for example, separately or mixed with the used lubricating oil that is fed to the distillation column. Unreacted borohydride reducing agent and other unwanted materials exit the distillation column as bottoms. In one embodiment, the borohydride reducing agent is present in an aqueous solution with sodium hydroxide and, when fed to a distillation column or evaporation unit, reduces the viscosity of the bottoms while reducing the temperature required to obtain a desired recovery of lubricating oil from the overhead fraction or fractions.
The present invention may be utilized either as a batch, semi-continuous or continuous process.
Care should be selected in the choosing of a particular borohydride reducing agent since some borohyride reducing agents are very unstable at elevated temperatures or slightly elevated temperatures and thus could pose a serious safety hazard if special precautions are not taken.
DETAILED DESCRIPTIONIn accordance with the invention, the used oil is contacted with at least one borohydride reducing agent. It is to be understood that by "contacting," included is any method by which the borohydride reducing agent contacts the used oil and the contaminants contained therein. Contact between the oil (including contaminants) and the borohydride reducing agent can be achieved by adding the borohydride directly to the used oil feedstock before any other treatment is begun. The used oil may be advantageously maintained at elevated temperature (greater than ambient temperature) during contact with the borohydride reducing agent because the rate of reaction between the borohydride reducing agent and contaminants increases as the temperature increases. However, the temperature should be lower than the decomposition temperature of the borohydride reducing agent. Accordingly, heating may be utilized to attain a desired temperature. Further, some type of agitation or mixing is desirable to further increase the rate of reaction. Preferably, the borohydride reducing agent is present in an aqueous solution with sodium hydroxide. The aqueous solution is contacted with the used oil and an oil phase and an aqueous phase forms. The aqueous phase, containing removed impurities and reaction products formed by contact between the used oil and borohydride reducing agent, is separated from the oil phase.
Most advantageously, the borohydride reducing agent is used in combination with a process for rerefining used oil either by evaporation or distillation in which the borohydride reducing agent is utilized to remove contaminants, including metal and carbonyl contaminants, from the used oil. In this embodiment, the borohydride reducing agent is preferably added to a distillation column or an evaporation unit as an aqueous solution with sodium hydroxide. This has the effect of reducing the distillation or evaporation temperature of the used oil and further provides a bottoms or residue product that is more fluid, facilitating pumping or other transport of the bottoms.
The distillation or evaporation should occur at a temperature lower than the decomposition temperature of the borohydride reducing agent utilized, to thereby prevent decomposition of the borohydride reducing agent.
Suitable evaporation processes are disclosed in U.S. patent application Ser. No. 202,019 and Ser. No. 202,018, both filed on Oct. 28, 1980 and entitled, respectively, "Method of Rerefining Used Lubricating Oil" and "Distillation and Solvent Extraction Process for Rerefining Used Lubricating Oil." It is to be understood that use of the present invention is not limited to use with evaporation, distillation or with the processes disclosed in the foregoing applications. Other processes may be used advantageously in conjunction with or as a modification of the invention. Processes which may be suitable are found in a book entitled "Reprocessing and Disposal of Waste Petroleum Oils" by L. Y. Hess published by Noyes Data Corporation.
Borohydride reducing agents that are suitable for use in accordance with the invention include the following compounds: sodium borohydride (NaBH.sub.4); potassium borohydride (KBH.sub.4); zinc borohydride (Zn(BH.sub.4)2); sodium cyanoborohydride (NaBH.sub.3 CN); sodium sulfurated borohydride (NaBH.sub.2 S.sub.3); lithium organo borohydride (LiBH(R).sub.3); sodium trioxyacetal borohydride (NaBH(OAc).sub.3); sodium trialkoxy borohydride (NaBH(OR).sub.3); sodium hydroxyl borohydride (NaBH.sub.3 (OH)); sodium borohydride anilide (NaBH.sub.3 (anilide)); tetrahydrofuran borohydride (THF.BH.sub.3); di-methyl-butyl borohydride ((3-Me-2-Bu).sub.2 BH); and lithium-aluminum hydride (LiAlH.sub.4). Mixtures of the foregoing borohydrides can also be utilized. However, in choosing among these various borohydride reducing agents care must be exercised so that use of a particular borohydride reducing agent does not present safety problems. Some borohydride reducing agents, such as lithium borohydride, decompose at relatively low temperatures and would therefore require processing at relatively low temperature to avoid decomposition.
In accordance with the preferred embodiment of the invention, the borohydride reducing agent is present in an aqueous solution containing an effective amount of sodium hydroxide for increasing the stability of the borohydride reducing agent.
Borohydride reducing agents which are preferred are sodium borohydride, potassium borohydride, and mixtures thereof. The most preferred borohydride reducing agent is sodium borohydride. Sodium borohydride is available commercially in powder, pellet and solution form. A preferred solution is an aqueous solution containing 12% by weight sodium borohydride and 41% by weight sodium hydroxide. Such a solution is commercially available from the Ventron Corporation of Beverly, Mass. and is marketed under the trademark "SWS."
The amount of borohydride reducing agent to be utilized can be determined by relating the amount of oxidized materials, metals and other components which are removed by treatment with the borohydride reducing agent. There is no minimum amount of borohydride reducing agent which can be utilized to improve the properties of the used oil, but a minimum amount would be required to react with essentially all of the reactable components that may be present in a given used oil. Generally, however, the amount of the 12% sodium borohydride/41% sodium hydroxide aqueous solution added to the used oil is between about 0.05% and 0.25% by volume of the used oil being treated.
The present invention and its advantages can be more completely understood by reference to the following examples:
EXAMPLE 1Distillation curves on waste oil utilizing the ANSI/ASTM Method D1160-77 entitled "Standard Method For Distillation of Petroleum Products at Reduced Pressure" with treatment utilizing sodium borohydride and without sodium borohydride were made. The waste oil was pre-distilled to remove fuel components and water.
Treatment with sodium borohydride was accomplished as follows. To 200 milliliters of waste oil was added 0.125% "SWS" solution (12% by weight sodium borohydride and 41% by weight sodium hydroxide obtained from Ventron Corporation) by volume (0.25 milliliters). The oil was placed in a 500 milliliter distillation flask to which had been added a magnetic stir bar. The oil was then distilled at a reduced pressure (10 mmHg) with the oil being stirred constantly.
The following are the results obtained, after correction to 760 mmHg:
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Distillation Temperature
Distillation Tempera-
with no sodium boro-
ture with sodium boro-
Percent hydride treatment
hydride treatment
Distilled
(degrees Fahrenheit)
(degrees Fahrenheit)
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Initial 517 548
boiling
point
10 648 671
20 718 738
30 767 799
40 813 844
50 851 873
60 887 889
70 924 936
80 996 982
90 1012 996
Ending point
1040 1015
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Thus, the distillation curve was lowered for the used lubricating oil that was treated with sodium borohydride after about 70% of the oil was distilled.
EXAMPLE 2Used lubricating oil was distilled utilizing two distillation processes, the difference being that one process was without treatment of the used lubricating oil with sodium borohydride, and the other process included treatment by sodium borohydride in the following manner. To 200 milliliters of waste oil was added 0.125% "SWS" solution (12% by weight sodium borohydride and 41% by weight sodium hydroxide obtained from Ventron Corporation) by volume (0.25 milliliters). The oil was placed in a 500 milliliter distillation flask to which had been added a magnetic stir bar. The oil was then distilled at a reduced pressure (10 mmHg) with the oil being stirred constantly.
A 100 SSU viscosity fraction was obtained from each process. The properties of each sample was as follows:
______________________________________
No sodium boro-
With sodium boro-
Property Hydride treatment
hydride treatment
______________________________________
Color 3+ 1.5
Neutralization number
0.3 0.01
(total acid number)
Copper corrosion test
4a 1A
Metals (ppm) 135 31
Odor Cracked (H.sub.2 S)
None
Carbonyl absorbance
0.55 0.022
(by infrared analysis)
Flash point (degrees F.)
350 365
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Thus, it can be seen that in the distillation process utilizing sodium borohydride treatment provided a distillate oil having properties which were substantially improved over the oil not treated with the sodium borohydride treatment.
While the invention has been described with respect to preferred embodiments, it is to be understood that the invention is capable of numerous alterations, rearrangements, combinations and other modifications, and those which are within the scope of the appended claims are intended to be covered thereby.
Claims
1. A method of rerefining used oil comprising contacting the used oil with at least one borohydride reducing agent.
2. The method as recited in claim 1 wherein the used oil is maintained at elevated temperature during contact with the borohydride reducing agent and below the decomposition temperature of said borohydride reducing agent.
3. The method as defined in claim 1 wherein said borohydride reducing agent is selected from the group consisting of sodium borohydride, potassium borohydride, and mixtures thereof.
4. The method as recited in claim 3 wherein the used oil is maintained at elevated temperature during contact with said borohydride reducing agent and below the decomposition temperature of said borohydride reducing agent.
5. The method as recited in claim 1 further comprising distillating or evaporating the used oil, said contacting step being performed before said distillation or evaporation.
6. The method as recited in claim 1 further comprising distillating or evaporating the used oil, said contacting step occurring during said distillation or evaporation.
7. The method as recited in claim 1 further comprising distillating or evaporating the used oil, said contacting step occurring after said distillation or evaporation.
8. The method as recited in claim 1 further comprising distillating or evaporating the used oil, said contacting step occurring before and during said distillation or evaporation.
9. The method as recited in claim 1 wherein said borohydride reducing agent is utilized as an aqueous solution of sodium hydroxide and said borohydride reducing agent.
10. The method as recited in claim 3 wherein said borohydride reducing agent is utilized as an aqueous solution of sodium hydroxide and sodium borohydride containing about 12% by weight sodium borohydride and about 41% by weight sodium hydroxide, said solution, including said borohydride reducing agent, being present in an amount between about 0.05% to about 0.25% by volume of the used oil.
11. The method as recited in claim 1 wherein said borohydride reducing agent is sodium borohydride present in an aqueous solution containing about 12% by weight sodium borohydride and about 41% by weight sodium hydroxide, said aqueous solution being present in an amount of between about 0.05% and 0.25% by volume of the used oil.
12. The method of claim 1 wherein said used oil is selected from the group consisting of lubricating oil, fuel oil, hydraulic oil, cutting oil, industrial oil, vegetable oil, synthetic oil and grease.
13. A method of increasing the flash point of used oil comprising contacting the used oil with an aqueous sodium hydroxide solution containing at least one borohydride reducing agent and thereafter separating the oil from the aqueous solution.
| 3008897 | November 1961 | Burk, Jr. et al. |
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| 3919076 | November 1975 | Cutter et al. |
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| 4366049 | December 28, 1982 | Knorre et al. |
| 4439311 | March 27, 1984 | O'Blasny |
Type: Grant
Filed: Feb 8, 1984
Date of Patent: Mar 12, 1985
Assignee: Delta Central Refining, Inc. (Natchitoches, LA)
Inventor: Richard H. O'Blasny (Natchitoches, LA)
Primary Examiner: Delbert E. Gantz
Assistant Examiner: Helane Myers
Law Firm: Jenner & Block
Application Number: 6/578,357
International Classification: C10G 710; C10G 700; C10M 1100;
